DE3939986A1 - Prodn. of foams of polystyrene or polyethylene - using chloro:di:fluoro:methane contg. ammonium bi:carbonate or other ammonium cpd. as blowing agent - Google Patents

Prodn. of foams of polystyrene or polyethylene - using chloro:di:fluoro:methane contg. ammonium bi:carbonate or other ammonium cpd. as blowing agent

Info

Publication number
DE3939986A1
DE3939986A1 DE19893939986 DE3939986A DE3939986A1 DE 3939986 A1 DE3939986 A1 DE 3939986A1 DE 19893939986 DE19893939986 DE 19893939986 DE 3939986 A DE3939986 A DE 3939986A DE 3939986 A1 DE3939986 A1 DE 3939986A1
Authority
DE
Germany
Prior art keywords
blowing agent
ammonium
polystyrene
contg
polyethylene
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
DE19893939986
Other languages
German (de)
Inventor
Erfinder Wird Nachtraeglich Benannt Der
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Gefinex GmbH
Original Assignee
Gefinex GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Gefinex GmbH filed Critical Gefinex GmbH
Priority to DE19893939986 priority Critical patent/DE3939986A1/en
Publication of DE3939986A1 publication Critical patent/DE3939986A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
    • C08J9/08Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
    • C08J9/127Mixtures of organic and inorganic blowing agents
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/14Saturated hydrocarbons, e.g. butane; Unspecified hydrocarbons
    • C08J2203/142Halogenated saturated hydrocarbons, e.g. H3C-CF3

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

In prepn of mouldings of polystyrene foam or polethylene foam, where the synthetic is plasticised in an extruder and mixed with a blowing agent which forms cells in the synthetic, the blowing agent is at least 50% of CHC1F2 (R22) contg 1-10 wt%, wrt the synthetic of (NH4)HC03 or an equiv amt of another NH4 cpd. Pref the amt of R22 is at least 85%. ADVANTAGE - Damage to the 03 layer is reduced to a value of 5-7, compared with a value of 100 for fluorocarbons. The amt of blowing agent is reduced by about 40%.

Description

Die Erfindung betrifft ein Verfahren zur Herstellung von Formkörpern aus Polystyrolschaum oder Polyethylenschaum, wobei Kunststoff im Extruder plastifiziert und mit einem Treibmittel gemischt wird, das im Kunststoff Zellen bildet, wobei das Treibmittel Chlordifuormethan (R 22) enthält.The invention relates to a process for the production of moldings made of polystyrene foam or polyethylene foam, plastic in Plasticized extruder and mixed with a blowing agent, which in the Plastic cells form, the blowing agent chlorodifuormethane (R 22) contains.

Aus der FR-PS 12 15 410 und US-PS 32 87 477 sind bereits Zellkörper auf Basis von alkenylaromatischen Polymerisaten bekannt, die unter Verwen­ dung von 1-Chlor 1,1,2,2,2-Pentafluoräthan als Treibmittel hergestellt worden sind. Dabei handelt es sich um Polystyrolschäume. Das Treib­ mittel steht ggf. in Mischung fluorierten und/oder chlorierten Verbin­ dungen oder Kohlenwasserstoffen.FR-PS 12 15 410 and US-PS 32 87 477 already have cell bodies Basis of alkenylaromatic polymers known under US tion of 1-chloro 1,1,2,2,2-pentafluoroethane as a blowing agent have been. These are polystyrene foams. The blowing medium is a mixture of fluorinated and / or chlorinated verbin or hydrocarbons.

Auch aus der DE-A 21 53 190 ist die Herstellung (Extrusion) länglicher Schaumstoffkörper aus thermoplastischen alkenylaromatischen Polymeren bekannt, wobei ein Treibmittelgemisch verwendet wird, welches 25 bis 75 Gew.-% Dichlordifluormethan, Trichlorfluormethan, Dichlortetra­ fluorethan oder Mischungen davon und 75 bis 25 Gew.-% Methylclorid, Äthylchlorid, Vinylchlorid oder Mischungen davon enthält.DE-A 21 53 190 also makes the production (extrusion) more elongated Foam body made of thermoplastic alkenyl aromatic polymers known, using a blowing agent mixture which is 25 to 75% by weight dichlorodifluoromethane, trichlorofluoromethane, dichlorotetra fluoroethane or mixtures thereof and 75 to 25% by weight methyl chloride, Contains ethyl chloride, vinyl chloride or mixtures thereof.

Mit dem Thema "Verminderung der Ozonschichtgefährdung" hat sich relativ früh die DE-PS 27 04 278 auseinandergesetzt. Dabei wurde die Erkenntnis offenbart, daß von einem Treibmittelgemisch aus
- 30 bis 70 Gew.-% 1.1-Difluor-1-Chlorethan und
- Methylchlorid, Ethylchlorid, Fluorchlormethan, Chlordifluormethan oder 1.1-Difluorethan
ausgegangen werden muß. Bei dieser Mischung wird das Dichlordifluor­ methan (R12) der oben beschriebenen anderen Treibmittelmischungen durch das 1.1-Difluor-1-Chlorethan ersetzt. Dies muß mehr oder weniger als zwangsläufiges Ergebnis einer Recherche zum Thema Ozongefährdung angesehen werden, denn ein US-Forschungsbericht, der IMOS-Report (Fluorcarbons and the Environment, Report of the Federal Task Force on Inadvertent Modifications of the Stratosphere) vom Juni 1975 schlägt vor, statt Frigen 12 weniger stabile Fluorkohlenwasserstoffe einzu­ setzen, insbesondere solche, die mehr als ein einziges Kohlenstoffatom und darüber hinaus noch Wasserstoffatome enthalten. Einer der einfach­ sten Vertreter dieser Stoffmasse ist das 1.1-Difluor-1-Chlorethan (R 142b). Der Grund für die geringere Ozonschichtgefährdung liegt darin, daß die weniger stabilen Fluorkohlenwasserstoffe durch Reaktion mit Hydroxyl-Radikalen entfernt werden.
DE-PS 27 04 278 dealt with the topic "Reduction of the Ozone Layer Hazard" relatively early. The finding was revealed that from a blowing agent mixture
- 30 to 70 wt .-% 1.1-difluoro-1-chloroethane and
- methyl chloride, ethyl chloride, fluorochloromethane, chlorodifluoromethane or 1.1-difluoroethane
must be assumed. In this mixture, the dichlorodifluoromethane (R12) of the other blowing agent mixtures described above is replaced by the 1,1-difluoro-1-chloroethane. This must be more or less seen as an inevitable result of research into ozone depletion, because a U.S. research report suggests the IMOS report (Fluorcarbons and the Environment, Report of the Federal Task Force on Inadvertent Modifications of the Stratosphere) from June 1975 , instead of using Frigen 12 less stable fluorocarbons, especially those that contain more than one carbon atom and also contain hydrogen atoms. One of the simplest representatives of this substance is 1.1-difluoro-1-chloroethane (R 142b). The reason for the lower risk to the ozone layer is that the less stable fluorocarbons are removed by reaction with hydroxyl radicals.

Aus den Auseinandersetzungen um das deutsche Patent 27 04 278 ist deutlich geworden, daß die dort vorgesehene spezielle Mischung als Auswahlerfindung angesehen werden kann. Dabei ist jedoch unberücksich­ tigt, daß diese Mischung mit den Mischungsbestandteilen R1 und R2 noch Fluorkohlenwasserstoffe mit hoher Ozonschichtgefährdung enthält.From the disputes over the German patent 27 04 278 is it became clear that the special mixture provided there as Selection invention can be viewed. However, this is not considered tends that this mixture with the mixture components R1 and R2 still contains fluorocarbons with a high risk of ozone layer.

Die Erfindung hat sich auch die Aufgabe gestellt, die Ozonschicht­ gefährdung zu verringern. Dabei geht die Erfindung von Versuchen aus, als Treibmittel R22 ohne R142b und auch ohne R11 oder R12 oder R14 zu verwenden. R11 ist ein Trichlorfluormethan, R14 Dichlor­ tetrafluoräthan, R12 ein Dichlordifluormethan. Die oben angeführten Verbindungen sind jeweils Abkömmlinge des Methans bzw. Äthans, wobei der Wasserstoff ganz oder teilweise durch Fluor bzw. Fluor und Chlor substituiert ist. Alle Verbindungen können der allgemeinen Formel unterstellt werden CmHnCltFq.The invention also has the task of reducing the ozone layer risk. The invention is based on attempts to use R22 without R142b as a blowing agent and also without R11 or R12 or R14. R11 is a trichlorofluoromethane, R14 dichlorotetrafluoroethane, R12 a dichlorodifluoromethane. The compounds listed above are in each case descendants of methane or ethane, the hydrogen being entirely or partially substituted by fluorine or fluorine and chlorine. All compounds can be assumed to have the general formula C m H n CltF q .

Dabei ist n + p + q = 2 m + 2 und m = der Zahl der Kohlenstoffatome, n = Zahl der Wasserstoffatome, p = der Zahl der Chloratome und q = der Zahl der Fluoratome.N + p + q = 2 m + 2 and m = the number of carbon atoms, n = Number of hydrogen atoms, p = the number of chlorine atoms and q = the Number of fluorine atoms.

Die oben angesprochenen R-Zeichen beinhalten unter Weglassung von p eine Numerierung in der Form HZE, wobei die Zahl H weggelassen wird, wenn sie Null ist. Es kennzeichnet:
H = m - 1 die Zahl der Kohlenstoffatome
Z = n + 1 die Zahl der Wasserstoffatome
E = q die Zahl der Fluoratome.
The R-characters mentioned above include a numbering in the form of HZE with the omission of p, the number H being omitted if it is zero. It features:
H = m - 1 the number of carbon atoms
Z = n + 1 the number of hydrogen atoms
E = q the number of fluorine atoms.

So ergeben sich z. B. für CCl2F2 (m = 1, n = 0, q = 2) R12 und CHCIF2 (m = 1, n = 1, q = 2) R22.So there are z. B. for CCl 2 F 2 (m = 1, n = 0, q = 2) R12 and CHCIF 2 (m = 1, n = 1, q = 2) R22.

Die mit Polyethylen durchgeführten Versuche brachten die Erkenntnis, daß R22 nur sehr schlecht mit Thermoplasten mischt. Der erzeugte Kunststoff hatte eine geringe Druckfestigkeit. Das wird darauf zurück­ geführt, daß das Material nach Verlassen des Extruders stark expan­ diert, wobei ca. 80% der Zellen zerstört werden bzw. sich zu großen Zellen vereinigen, die nicht mehr geschlossenzellig sind.The tests carried out with polyethylene that R22 mixes very poorly with thermoplastics. The generated one Plastic had a low compressive strength. That will go back to that led that the material expan strongly after leaving the extruder dated, whereby about 80% of the cells are destroyed or become too large Merge cells that are no longer closed cells.

Bei Zugabe wesentlicher Mengen von R142b sind die oben beschriebenen Nachteile nicht mehr zu beobachten. Allerdings beträgt die Menge an R142b in gängigen Treibmittelmischungen immer ein Vielfaches der Menge von R22. Gleichwohl sieht die Erfindung in R142b nur ein Additiv, welches die Wirkung von R22 zur Entfaltung bringt. Vor diesem Hintergrund hat sich die Erfindung die Aufgabe gestellt, R22 mit einem anderen Additiv zur Wirkung zu bringen. Dabei hat sich der Erfinder erinnert, daß die Treibmittel R11, R12, R22 usw. ursprüng­ lich Kältemittel waren und das früher als Kältemittel benutzte Ammoniak abgelöst haben. Zwar kann auch Ammoniak als Treibmittel verwendet werden. Mit Ammoniak ergeben sich jedoch sehr schlechte Oberflächen am Schaum. Die einzelnen Blasen (Zellen) bilden sich kugelig aus, so daß eine sehr rauhe Oberfläche entsteht. Gleichwohl beinhaltet die Erfindung den Entschluß, Ammoniak zusammen mit R22 und der Maßgabe einzusetzen, die oben beschriebene Additiv-Wirkung herbei­ zuführen. Das Ammoniak kann in verschiedenen Formen zugesetzt werden, flüssig, in Wasser gelöst als Salmiakgeist oder pulverförmig, z. B. als Ammonium-Bicarbonat. Nach der Erfindung wird von dem pulverförmi­ gen Ammonium-Carbonat 1 bis 10 Gew.-% bezogen auf das Thermoplast Polyethylen oder Poylstyrol zugegeben. Im übrigen wird das Treibmittel durch R22 gebildet. Soweit Additive zum Einsatz kommen, bleiben diese unverändert. Additive sind z. B. Talk als Keimbildner und Mittel, welche den Schrumpf des Schaums hindern. Solche Schrumpfhemmer sind z. B. Fettsäureamide. Ganz besonders vorteilhafte und bislang nicht bekannte Wirkungen haben Mischungen aus Glycerin (3 bis 7%) und Monoglyceride (36 bis 40%) und Seife.When substantial amounts of R142b are added, those described above are Disadvantages no longer observed. However, the amount is R142b in common blowing agent mixtures always a multiple of Amount of R22. Nevertheless, the invention only looks at R142b Additive that unfolds the effects of R22. In front Against this background, the invention has the task of R22 with another additive. The The inventor recalls that the blowing agents R11, R12, R22, etc. originally were refrigerants and used to be used as refrigerants Detached ammonia. Ammonia can also be used as a blowing agent be used. With ammonia, however, very bad results Surfaces on the foam. The individual bubbles (cells) form spherical, so that a very rough surface is created. Nevertheless the invention includes the decision ammonia together with R22 and the proviso to use the additive effect described above respectively. The ammonia can be added in various forms, liquid, dissolved in water as ammonia or powder, e.g. B. as ammonium bicarbonate. According to the invention of the powder ammonium carbonate 1 to 10 wt .-% based on the thermoplastic Polyethylene or polystyrene added. Otherwise, the blowing agent formed by R22. If additives are used, they remain unchanged. Additives are e.g. B. talc as a nucleating agent and agent,  which prevent the foam from shrinking. Such shrink inhibitors are e.g. B. fatty acid amides. Very particularly advantageous and so far not known effects have mixtures of glycerol (3 to 7%) and Monoglycerides (36 to 40%) and soap.

Ammonium-Bicarbonat-Pulver hat die Handelsbezeichnung Hirschhornsalz. Seine chemische Formel ist NH4HCO3. Ammonium-Bicarbonat zerfällt bei Erwärmen im Extruder in Ammoniak, Kohlendioxid und Wasser. Der Ammoniakanteil ist ca. 21,5%, der Kohlendioxidanteil ca. 55,7%. Neben dem Wasser ergeben sich noch geringfügige andere Rückstände.Ammonium bicarbonate powder has the trade name Hirschhornsalz. Its chemical formula is NH 4 HCO 3 . When heated in the extruder, ammonium bicarbonate breaks down into ammonia, carbon dioxide and water. The ammonia content is approx. 21.5%, the carbon dioxide content approx. 55.7%. In addition to the water, there are minor other residues.

Anstelle des pulverförmigen Ammonium-Bicarbonats können auch Ammoniak bzw. andere Ammoniakverbindungen in äquivalenter Menge verwendet werden.Instead of the powdered ammonium bicarbonate, ammonia can also be used or other ammonia compounds used in an equivalent amount will.

Bei erfindungsgemäßer Anwendung eines im wesentlichen aus R22 be­ stehenden Treibmittels reduziert vorteilhafterweise der notwendige Gasanteil im Schaum um etwa 40% gegenüber einem Herstellungsvorgang mit R11, R12 oder R114. Das hat eine weitere sehr vorteilhafte Verringerung der Ozonschichtgefährdung zur Folge. Bei Bemessung der Ozonschichtgefährdung mit der Wertzahl 100 für gefährliche Fluor­ kohlenwasserstoffe geht von dem R22 lediglich eine Gefährdung mit der Wertzahl 5 bis 7 aus, die sich noch mal entsprechend der 40%igen Reduzierung des Gasanteiles reduziert, so daß im Ergebnis mit dem R22 eine Reduzierung auf die Wertzahl 3 bis 4 erreicht wird.When using an essentially from R22 standing propellant advantageously reduces the necessary Gas content in the foam by about 40% compared to a manufacturing process with R11, R12 or R114. That has another very beneficial one Reduction of the risk to the ozone layer. When dimensioning the Ozone layer hazard with the value number 100 for dangerous fluorine hydrocarbons is only a hazard with the R22 Value number 5 to 7 from, which again according to the 40% Reduction of the gas portion reduced, so that as a result with the R22 a reduction to the value number 3 to 4 is achieved.

Claims (2)

1. Verfahren zur Herstellung von Formkörpern aus Polystyrolschaum oder Polyethylenschaum, wobei der Kunststoff im Extruder plastifiziert und mit einem Treibmittel gemischt wird, das im Kunststoff Zellen bildet, wobei als Treibmittel R22 verwendet wird, dadurch gekenn­ zeichnet, daß der Anteil an R22 mindestens 50% beträgt und dem R22 von 1 bis 10 Gew.-% Ammonium-Bicarbonat, bezogen auf den eingesetzten Kunststoff oder eine andere Ammoniakverbindung in äquivalenter Menge zugeordnet ist.1. A process for the production of molded articles made of polystyrene foam or polyethylene foam, the plastic being plasticized in the extruder and mixed with a blowing agent which forms cells in the plastic, R22 being used as blowing agent, characterized in that the proportion of R22 is at least 50% is and the R22 is assigned from 1 to 10 wt .-% ammonium bicarbonate, based on the plastic used or another ammonia compound in an equivalent amount. 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß die Menge an R22 im Treibmittel mindestens 85% beträgt.2. The method according to claim 1, characterized in that the amount of R22 in the blowing agent is at least 85%.
DE19893939986 1989-12-02 1989-12-02 Prodn. of foams of polystyrene or polyethylene - using chloro:di:fluoro:methane contg. ammonium bi:carbonate or other ammonium cpd. as blowing agent Withdrawn DE3939986A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE19893939986 DE3939986A1 (en) 1989-12-02 1989-12-02 Prodn. of foams of polystyrene or polyethylene - using chloro:di:fluoro:methane contg. ammonium bi:carbonate or other ammonium cpd. as blowing agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19893939986 DE3939986A1 (en) 1989-12-02 1989-12-02 Prodn. of foams of polystyrene or polyethylene - using chloro:di:fluoro:methane contg. ammonium bi:carbonate or other ammonium cpd. as blowing agent

Publications (1)

Publication Number Publication Date
DE3939986A1 true DE3939986A1 (en) 1991-06-06

Family

ID=6394734

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19893939986 Withdrawn DE3939986A1 (en) 1989-12-02 1989-12-02 Prodn. of foams of polystyrene or polyethylene - using chloro:di:fluoro:methane contg. ammonium bi:carbonate or other ammonium cpd. as blowing agent

Country Status (1)

Country Link
DE (1) DE3939986A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011110613A1 (en) * 2011-08-16 2013-02-21 Frank van Lück Extruded foamed web manufacturing method for foamed product used as e.g. rock wool on roof region for thermal insulation, involves cooling interior of body by internal cooling flow so that specific thickness tolerance of web is obtained

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1215410A (en) * 1957-11-29 1960-04-19 Dow Chemical Co A method of making a latently foaming polymerized composition
US3287477A (en) * 1964-11-12 1966-11-22 Koppers Co Inc Process and apparatus for extruding a foamed plastic
DE1808364A1 (en) * 1967-11-15 1969-07-24 Haveg Industries Inc Process for the production of thermoplastic foams
DE2153190A1 (en) * 1970-10-29 1972-05-04 Dow Chemical Co Alkeny! Aromatic polymer foam and process for its manufacture
DE2704278C2 (en) * 1976-02-03 1983-08-04 The Dow Chemical Co., 48640 Midland, Mich. Process for producing an alkenyl aromatic, thermoplastic, synthetic, resinous, elongated foam body
DE3800650A1 (en) * 1988-01-12 1989-07-20 Marquet & Cie Noel Process for the preparation of foamed plastics

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1215410A (en) * 1957-11-29 1960-04-19 Dow Chemical Co A method of making a latently foaming polymerized composition
US3287477A (en) * 1964-11-12 1966-11-22 Koppers Co Inc Process and apparatus for extruding a foamed plastic
DE1808364A1 (en) * 1967-11-15 1969-07-24 Haveg Industries Inc Process for the production of thermoplastic foams
DE2153190A1 (en) * 1970-10-29 1972-05-04 Dow Chemical Co Alkeny! Aromatic polymer foam and process for its manufacture
DE2704278C2 (en) * 1976-02-03 1983-08-04 The Dow Chemical Co., 48640 Midland, Mich. Process for producing an alkenyl aromatic, thermoplastic, synthetic, resinous, elongated foam body
DE3800650A1 (en) * 1988-01-12 1989-07-20 Marquet & Cie Noel Process for the preparation of foamed plastics

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102011110613A1 (en) * 2011-08-16 2013-02-21 Frank van Lück Extruded foamed web manufacturing method for foamed product used as e.g. rock wool on roof region for thermal insulation, involves cooling interior of body by internal cooling flow so that specific thickness tolerance of web is obtained
DE102011110613B4 (en) * 2011-08-16 2017-06-14 Frank van Lück Process for the production of an extruded foam sheet and foam produced by this process

Similar Documents

Publication Publication Date Title
DE69120929T2 (en) Foaming thermoplastic elastomers
DE69730122T2 (en) STABILITY CONTROL COMPOSITION FOR POLYOLEFINE FOAM
DE69931569T2 (en) Biodegradable steam corrosion inhibitors
DE2423767A1 (en) PUTTING ADHESIVES, SEALING COMPOUNDS, CLAMPING COMPOUNDS, COVERING COMPOUNDS AND SIMILAR KIT PRODUCTS WITH RESISTANT, ORGANIC MICROBALLS AND PROCESS FOR THEIR PRODUCTION
DE3242827A1 (en) POLYOLEFINE-BASED POLYMER DIMENSIONS
DE2537232B2 (en) INJECTION AND MOLDING COMPOUND
DE2655710A1 (en) PRIMER COMPOSITION AND METHOD OF USING THIS COMPOSITION
DE1966141A1 (en) Process for producing an ethylene resin foam
DE2911719A1 (en) METHOD FOR PRODUCING LIGHTWEIGHT FOAM FROM THERMOPLASTIC CRYSTALLINE PLASTICS
DE1794182B2 (en) Flame-retardant molding compounds made from styrene polymers
DE2037027A1 (en) Process for the production of foam bodies
DE3939986A1 (en) Prodn. of foams of polystyrene or polyethylene - using chloro:di:fluoro:methane contg. ammonium bi:carbonate or other ammonium cpd. as blowing agent
DE2103198A1 (en) Propellant
EP0256967B1 (en) Composition for the preparation of moulded articles
DE69123150T2 (en) ANTISTATIC POLYOLEFINE FOAMS AND FILMS AND METHOD FOR PRODUCING THE FOAM AND THE ANTISTATIC COMPOSITION
DE69319984T2 (en) Stabilized compositions containing fluorocarbons, premixes for the production of polymer foams and polymer foams obtained
DE2853445A1 (en) COMPOSITION FOR TREATING A FOAM SUBSTRATE WITH CLOSED CELLS
DE3930594A1 (en) Moulded foam prods., esp. of polystyrene foam - by extrusion, using mixt. of above 30 wt. per cent 1,1-di:fluoro-1-chloro-ethane and water and-or nitrogen as blowing agent
DE1920931A1 (en) Foamable polymer compositions and the foam bodies made from them
DE1469899A1 (en) Flame retardant plastics
DE1669998C3 (en) Self-extinguishing ethylene copolymer foams
DE3139401C2 (en) Stabilizing polyether or polyester molding compounds against premature reactions
DE2359007A1 (en) EXPANDABLE THERMOPLASTIC PREPARATIONS
DE3002582A1 (en) COMPOSITION WITH PHOSPHORESCENT EFFECT
EP0060532B1 (en) Anti-catalytic additives for fire retardant and fire extinguishing powders, these powders and method of their preparation

Legal Events

Date Code Title Description
8181 Inventor (new situation)

Free format text: KOLOSSOW, KLAUS-DIETER, 3107 HAMBUEHREN, DE

8110 Request for examination paragraph 44
8130 Withdrawal